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Consistent inventory control ,† †, Elvira Marie B. Aske, andSigurd Skogestad Department of Chemical Engineering, Norwegian University of Science and Technology, Trondheim, Norway Abstract Inventory or material balance control is an important part of process control. In the litera- ture, many rules have been proposed to help in designing such systems, but their justification is often unclear. The main contribution of this paper is to propose the more general local- consistency rule for evaluating inventory control systems. Consistency means that the steady- state mass balances (total, component and phase) for the individual units and the overall plant are satisfied. In addition, local-consistency is a desired property, meaning that the local mass balances are satisfied with local inventory loops only. Introduction One of the more elusive aspects of process control education is inventory or material balance control. An engineer with some experience can usually immediately say if a proposed inventory control system is workable. However, for a student or newcomer to the field, it is not obvious, and even for an experienced engineer there may be cases where experience and intuition are not sufficient. The objective of this paper is to present concise results on inventory control, relate to previous work, tie up loose ends, and to provide some good illustrative examples. The main result †Norwegian University of Science and Technology ‡Current address: StatoilHydro Research Centre, Trondheim, Norway 1 (consistency rule) can be regarded as obvious, but nevertheless we have not seen it presented in this way before. The main result is a simple rule to check whether an inventory control system is consistent. Here, consistency means that the mass balances for the entire plant and units are satisfied.1 In ∗ addition, we usually want the inventory control system to be local-consistent. Local-consistency requires, in addition to consistency, that all inventories are regulated locally, without the need to rely on control loops outside the unit. Consistency is a required property, because the mass bal- ances must be satisfied in a plant, whereas local-consistency is a desirable property of an inventory control system. In practice, an inconsistent control structure will lead to a situation with a fully open or closed control valve and the associated control loop cannot fulfill or attain the control set point.3 In most plants, we want the inventory control system to use simple PI controllers and be part of the basic (regulatory) control layer. This is because it is generally desirable to separate the tasks of regulatory (stabilizing) control and supervisory (economic) control. From this it follows that the structure of the inventory control system is usually difficult to change later. Theimportanceofconsistencyofinventory control structures is often overlooked. Our work is partly inspired by the many examples of Kida, who has given industrial courses in Japan on control structures for many years. In a personal communication3 he states that “most process engineers, and even academic people, do not understand the serious problem of inconsistency of plantwide control configurations. When writing a paper, you have to clearly explain this point and make them convinced at the very outset. Otherwise they will not listen to or read through your detailed statements, but skip them all”. Averygoodearlyreference on inventory control in a plantwide setting is Buckley.4 He states that material balance control must be in the direction of flow downstream a given flow and opposite the direction of flow upstream a given flow. Price et. al1,2 extended this and state that the inventory controlmust“radiate”outwardsfromthepointofagivenflow(throughputmanipulator). Asshown ∗“Local-consistency” is closely related to the term “self-consistency” used by Price and Georgakis.1,2 2 in this paper, these statements are a consequence of requiring the inventory control system to be local-consistent. Downs5 provides a very good discussion of material balance control in a plantwide control environment, with many clarifying examples. However, it is somewhat difficult for the reader to findageneral rule or method that can be applied to new cases. Luyben et al.6 propose a mainly heuristic design procedure for plantwide control. Luyben’s procedure consists of, among others, “Step 6. Control inventories (pressures and levels) and fix a flow in every recycle loop”. Possible limitations of this guideline are discussed in the present paper. Another guideline of Luyben et al.6 is to “ensure that the overall component balances for each chemical species can be satisfied either through reaction or exit streams by accounting for the component’s composition or inventory at some point in the process”. This guideline is a bit limited because entrance (feed) streams is not considered. Specific guidelines for designing inventory control structures are presented by Price and Geor- gakis.1,2 They propose a set of heuristic guidelines for inventory control design in a plantwide environment and also discuss consistency. The authors also state the importance of a consistent in- ventory control structure: “Self-consistency appears to be the single most important characteristic governing the impact of the inventory control structure on system performance”. Asalreadymentioned,FujioKidafromJGCCorporationinJapanhasdevelopedalotofteach- ing material3 and written several papers on inventory control.7 Unfortunately, the work is pub- lished in Japanese only, but nevertheless it is clear that there are many detailed rules and some require detailed calculations. In summary, the literature provides a number of specific rules of designing inventory control systems, but the justification and limitations of these rules are often unclear. The main result of this paper is to present the simple local-consistency rule for evaluating inventory control systems, which applies to all cases and only requires structural information. The outline of the paper is as follows. First the terms consistency and local-consistency are defined, then we present and derive the local-consistency rule. We then apply the rule to some 3 flownetworks,suchasunitsinseries and recycle system. This is followed by a derivation of some more specific rules before we end up with some more complex examples, including distillation and recycle reactors. Note that the present paper focuses on analysis of a given control structure. The design of the inventory control system, which in particular is related to the placement of the throughput manipulator, is discussed in more detail in Aske8.9 Remark on notation: In this paper, when a flow (valve) is left unused or with a flow controller (FC), then this indicates that this is a given flow. By the term "given flow" we mean that the flow is not used for inventory control but rather given by conditions outside the inventory control system. Specifically, in this paper a "given flow" can be 1. a throughput manipulator (TPM), 2. a flow that comes from another part of the plant (disturbance for our part), 3. a fixed flow 4. a flow that is used for other control tasks (eg., control of composition or temperature). Definition of consistent inventory control The dynamic mass balance for total or component mass in any unit or process section can be written:5 dI =Rateofchangeininventory = Inflow + Generation - Outflow - Consumption (1) dt During operation we must have “inventory regulation”, meaning that the inventories of total, com- ponent and phase mass are kept within acceptable bounds. To achieve this we need a “consistent” and preferably “local-consistent” inventory control system. Definition 1. Consistency. An inventory control system is consistent if it can achieve acceptable inventory regulation for any part of the process, including the individual units and the overall 4
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